Set the average and peak flow, influent TSS and the design basis, and get the surface area, detention time,
weir overflow rate, TSS/BOD removal and the primary-sludge volume — the first solids-liquid step of the train.
Includes a tropical note on when a PST is worth the land, and when SEA plants sensibly skip it.
1Duty & design basis
Average flow sets the surface area; peak flow sets the check. In warm SEA cities peak factors run 2–2.5.
Results — sizing & removal
Surface area A
—m²
Detention HRT
—h
Peak SOR
—m/h
Item
Value
Basis
2Removal & sludge
Primary sludge is ~3–6 % DS; this sheet uses 5 % (50 kg DS/m³) and a 25–35 % BOD pull-down linked to TSS removal.
Stream
kg/d
m³/d
The BOD removed here subtracts directly from the aeration load downstream — feed it into the A²/O or oxidation-ditch tool.
Tropical verdict
Quote the PST instruments at factory price
A clarifier needs few instruments — but the ones it needs ( sludge-blanket level, RAS flow, inlet TSS/flow pacing)
are exactly what we supply at the manufacturer's ex-works price. Our margin is the export tax rebate only.
Primary sludge ~ 0.1 m³/PE·d, 3–6 % DS; this sheet uses 5 % (50 kg DS/m³) for volume.
Full derivation and worked example: Primary-Clarifier-Calculation-Sheet.md. The basis switch changes only the SOR / weir envelope — the settling physics is identical, and the alternative basis is always shown.